WO2012066889A1 - ガラス板の製造装置およびガラス板の製造方法 - Google Patents

ガラス板の製造装置およびガラス板の製造方法 Download PDF

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Publication number
WO2012066889A1
WO2012066889A1 PCT/JP2011/073736 JP2011073736W WO2012066889A1 WO 2012066889 A1 WO2012066889 A1 WO 2012066889A1 JP 2011073736 W JP2011073736 W JP 2011073736W WO 2012066889 A1 WO2012066889 A1 WO 2012066889A1
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WO
WIPO (PCT)
Prior art keywords
glass
glass ribbon
glass plate
chamber
manufacturing apparatus
Prior art date
Application number
PCT/JP2011/073736
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English (en)
French (fr)
Japanese (ja)
Inventor
哲史 瀧口
督博 鏡味
Original Assignee
旭硝子株式会社
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 旭硝子株式会社 filed Critical 旭硝子株式会社
Priority to EP11841009.1A priority Critical patent/EP2641881A4/en
Priority to KR1020127018008A priority patent/KR101223395B1/ko
Priority to CN201180055637.5A priority patent/CN103221352B/zh
Priority to JP2012523147A priority patent/JP5838966B2/ja
Publication of WO2012066889A1 publication Critical patent/WO2012066889A1/ja

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    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B18/00—Shaping glass in contact with the surface of a liquid
    • C03B18/02—Forming sheets
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B25/00—Annealing glass products
    • C03B25/04—Annealing glass products in a continuous way
    • C03B25/06—Annealing glass products in a continuous way with horizontal displacement of the glass products
    • C03B25/08—Annealing glass products in a continuous way with horizontal displacement of the glass products of glass sheets
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B18/00—Shaping glass in contact with the surface of a liquid
    • C03B18/02—Forming sheets
    • C03B18/18—Controlling or regulating the temperature of the float bath; Composition or purification of the float bath
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B18/00—Shaping glass in contact with the surface of a liquid
    • C03B18/02—Forming sheets
    • C03B18/20—Composition of the atmosphere above the float bath; Treating or purifying the atmosphere above the float bath
    • C03B18/22—Controlling or regulating the temperature of the atmosphere above the float tank
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B35/00—Transporting of glass products during their manufacture, e.g. hot glass lenses, prisms
    • C03B35/14—Transporting hot glass sheets or ribbons, e.g. by heat-resistant conveyor belts or bands
    • C03B35/16—Transporting hot glass sheets or ribbons, e.g. by heat-resistant conveyor belts or bands by roller conveyors
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B18/00—Shaping glass in contact with the surface of a liquid
    • C03B18/02—Forming sheets
    • C03B18/16—Construction of the float tank; Use of material for the float tank; Coating or protection of the tank wall

Definitions

  • the present invention relates to a glass plate manufacturing apparatus and a glass plate manufacturing method.
  • the float method is known as one of the typical methods for producing a glass plate.
  • molten glass is continuously supplied to a bath surface of molten metal (for example, molten tin) in a float bath to form a strip-shaped glass ribbon.
  • molten metal for example, molten tin
  • the glass ribbon is transported into a slow cooling furnace and gradually cooled while being transported on a transport roll.
  • the glass ribbon is carried out of the slow cooling furnace, cooled to near room temperature, and then cut into a predetermined dimension to become a glass plate as a product.
  • the glass ribbon may be exposed to the outside air between the float bath and the slow cooling furnace, and may be affected by the temperature. As a result, the glass ribbon is deformed and may remain as a warp in the product even if the temperature distribution in the slow cooling furnace is optimized.
  • the device for adjusting the temperature distribution is configured by a heater, a pipe, and the like.
  • the heaters are spaced apart on the upper and lower sides of the glass ribbon, and are fixed to the inner wall of the chamber.
  • a plurality of heaters are provided in the glass ribbon transport direction.
  • the heaters in each row are divided in the width direction of the glass ribbon, and the temperature of the glass ribbon is controlled to be uniform in the width direction.
  • the pipe is provided on the upstream side in the chamber, and injects an inert gas such as nitrogen near the center of the lower surface of the glass ribbon.
  • an inert gas such as nitrogen near the center of the lower surface of the glass ribbon.
  • the temperature distribution in the conveyance direction of the glass ribbon may not be optimized. In that case, even if the temperature distribution of the glass ribbon is optimized in the slow cooling furnace, it is difficult to eliminate the warp of the product.
  • glass substrates having a small thickness have been manufactured for display panels such as a liquid crystal display (LCD) and a plasma display (PDP).
  • LCD liquid crystal display
  • PDP plasma display
  • This invention was made in view of the said subject, Comprising: It aims at providing the manufacturing apparatus of the glass plate which can suppress the curvature of a product, and the crack of a glass ribbon, and the manufacturing method of a glass plate.
  • the glass plate manufacturing apparatus of the present invention comprises: A float bath containing molten metal, a slow cooling furnace into which a glass ribbon formed into a plate shape on the molten metal is carried, a chamber provided between the float bath and the slow cooling furnace, and provided in the chamber A glass plate manufacturing apparatus comprising a plurality of lift-out rolls for transporting the glass ribbon from the float bath to the slow cooling furnace, In the chamber, a first supply air for supplying an inert gas as a cooling gas to a space downstream of a contact point between the glass ribbon and the most downstream lift-out roll in a lower space of the glass ribbon. With units.
  • a plurality of transport rolls that are provided in the slow cooling furnace and transport the glass ribbon
  • a second air supply for supplying a cooling gas to a space upstream of a contact point between the glass ribbon and the most upstream transport roll in a lower space or / and an upper space of the glass ribbon. It is preferable to provide a unit.
  • the cooling gas supplied by the second air supply unit includes at least one of air, water vapor, and inert gas.
  • an inert gas is disposed in a space upstream of the contact point between the glass ribbon and the most upstream lift-out roll. It is preferable to further include a third air supply unit for supplying the air.
  • the contact point between the glass ribbon and the most upstream lift-out roll, and the glass ribbon and the most downstream lift in the chamber, in the lower space of the glass ribbon, the contact point between the glass ribbon and the most upstream lift-out roll, and the glass ribbon and the most downstream lift. It is preferable to further include a fourth air supply unit that supplies an inert gas in at least a part of the space between the contact point with the out-roll.
  • the glass plate manufacturing apparatus of the present invention preferably further includes a fifth air supply unit for supplying an inert gas from the vicinity of the upper wall of the outlet of the float bath to the lower side in the chamber.
  • a member for partitioning an upper space of the glass ribbon is further provided in the chamber above the glass ribbon.
  • a heater is further provided in the chamber.
  • a heater is preferably provided in the vicinity of the outlet in the float bath.
  • a heater is provided in the vicinity of the inlet in the slow cooling furnace.
  • the inert gas supplied by the first air supply unit is preferably nitrogen gas.
  • the inert gas supplied by the second air supply unit is preferably nitrogen gas.
  • the inert gas supplied by the third air supply unit is preferably nitrogen gas.
  • the inert gas supplied by the fourth air supply unit is preferably nitrogen gas.
  • the inert gas supplied by the fifth air supply unit is preferably nitrogen gas.
  • a detector for detecting cracks in the glass ribbon is provided near the outlet in the chamber or near the inlet in the slow cooling furnace.
  • the chamber preferably has a heat insulating structure.
  • the manufacturing method of the glass plate of this invention is as follows. Molten glass is continuously supplied to the molten metal bath surface in the float bath to form a strip-shaped glass ribbon, the glass ribbon is transported from the float bath into the chamber, and a plurality of lifts are formed in the chamber. A method for producing a glass sheet that is conveyed on an out-roll, and then gradually cooled in a slow cooling furnace, In the chamber, an inert gas is supplied as a cooling gas to a space downstream of the contact point between the glass ribbon and the most downstream lift-out roll in the lower space of the glass ribbon.
  • the glass plate is preferably alkali-free glass.
  • the glass plate is an oxide-based mass percentage display, SiO 2 : 50 to 66% Al 2 O 3 : 10.5-24% B 2 O 3 : 0 to 12% MgO: 0-8% CaO: 0 to 14.5% SrO: 0-24% BaO: 0 to 13.5% MgO + CaO + SrO + BaO: 9 to 29.5% ZrO 2 : 0 to 5% It is preferable that it contains.
  • the glass plate is an oxide-based mass percentage display, SiO 2 : 58 to 66% Al 2 O 3 : 15-22% B 2 O 3 : 5-12% MgO: 0-8% CaO: 0-9% SrO: 3 to 12.5% BaO: 0-2% MgO + CaO + SrO + BaO: 9-18% It is preferable that it contains.
  • the present invention it is possible to provide a glass plate manufacturing apparatus and a glass plate manufacturing method capable of suppressing product warpage and glass ribbon cracking.
  • FIG. 1 is a partial cross-sectional view of a glass plate manufacturing apparatus according to a first embodiment of the present invention.
  • downstream refers to the downstream in the conveyance direction of the glass ribbon
  • upstream refers to the upstream in the conveyance direction of the glass ribbon
  • FIG. 1 is a partial cross-sectional view of a glass plate manufacturing apparatus according to an embodiment of the present invention.
  • the glass plate manufacturing apparatus 1 includes a float bath 10, a slow cooling furnace 20, and a chamber 30 provided between the float bath 10 and the slow cooling furnace 20.
  • the glass ribbon 2 formed to have a desired width and thickness on the bath surface 12 of the molten metal 11 in the float bath 10 is pulled up from the bath surface 12 by the pulling force of the lift-out rolls 41 to 43 and the transport rolls 21 and 22. It is done.
  • the glass ribbon 2 is carried into the chamber 30 from the outlet 13 of the float bath 10 and conveyed on the lift-out rolls 41 to 43.
  • the glass ribbon 2 is carried into the slow cooling furnace 20 and gradually cooled while being transported on the transport rolls 21 and 22. Thereafter, the glass ribbon 2 is carried out of the slow cooling furnace 20 and cooled to near room temperature, and then cut into a predetermined size to form a glass plate as a product.
  • the glass used for the glass plate is appropriately selected according to the use of the glass plate. For example, when the glass plate is used for a plasma display, soda lime glass having a high strain point temperature and a large thermal expansion coefficient is used. Further, when the glass plate is used for a liquid crystal display, an alkali metal adversely affects the quality of the liquid crystal display, and therefore, an alkali-free glass that does not substantially contain an alkali metal is used.
  • non-alkali glass refers to a glass that does not intentionally contain an alkali metal oxide such as Li 2 O, Na 2 O, or K 2 O.
  • the apparatus for producing a glass plate according to the present invention is particularly suitable for the production of alkali-free glass, with the oxide-based mass percentage display, SiO 2 : 50 to 66% Al 2 O 3 : 10.5-24% B 2 O 3 : 0 to 12% MgO: 0-8% CaO: 0 to 14.5% SrO: 0-24% BaO: 0 to 13.5% MgO + CaO + SrO + BaO: 9 to 29.5% ZrO 2 : 0 to 5% It is more preferable when it is an alkali-free glass containing.
  • the alkali-free glass is expressed in terms of mass percentage based on oxide, SiO 2 : 58 to 66% Al 2 O 3 : 15-22% B 2 O 3 : 5-12% MgO: 0-8% CaO: 0-9% SrO: 3 to 12.5% BaO: 0-2% MgO + CaO + SrO + BaO: 9-18% Is more preferable when it contains.
  • the glass ribbon 2 is formed by charging a plurality of types of raw materials corresponding to a glass plate into a melting tank to prepare molten glass, and continuously supplying the molten glass into the float bath 10. Before supplying the molten glass into the float bath 10, it is desirable to defoam bubbles contained in the molten glass.
  • the float bath 10 contains a molten metal 11.
  • the upper space in the float bath 10 is filled with a reducing gas containing nitrogen and hydrogen in order to prevent the molten metal 11 from being oxidized.
  • the upper space in the float bath 10 is set to a pressure higher than the atmospheric pressure in order to prevent the inflow of air from the outside.
  • a heater 18 for adjusting the glass ribbon 2 to a temperature capable of plastic deformation is provided.
  • the amount of heat generated by the heater 18 may be automatically controlled based on the temperature near the outlet 13 in the float bath 10. For example, the temperature in the vicinity of the outlet 13 in the float bath 10 is detected by a temperature sensor such as a thermocouple, and the detection result is supplied to a control device including a microcomputer. The control device automatically controls the amount of heat generated by the heater 18 based on the detection result of the temperature sensor. Similarly, the amount of heat generated by heaters 28 and 48 described later may be automatically controlled.
  • the temperature of the glass ribbon 2 in the vicinity of the outlet 13 in the float bath 10 is appropriately set according to the type of glass and the like. For example, a temperature higher by 32 to 78 ° C. based on the annealing point of the glass is preferable.
  • the annealing point of the glass is a temperature at which the viscosity of the glass is 10 13 dPa ⁇ s, and is determined by the composition of the glass.
  • the slow cooling furnace 20 is opened to the outside at the downstream outlet. Therefore, the inside of the slow cooling furnace 20 is basically an air atmosphere.
  • the inside of the slow cooling furnace 20 communicates with the inside of the float bath 10 through the inside of the chamber 30.
  • a heater 28 and the like are provided in addition to the transfer rolls 21 and 22.
  • Each of the transport rolls 21 and 22 is rotationally driven by a driving device such as a motor, and transports the glass ribbon 2 in the horizontal direction by the driving force.
  • the heater 28 is provided near the inlet 23 in the slow cooling furnace 20.
  • the heater 28 is provided above and / or below the glass ribbon 2.
  • the temperature of the glass ribbon 2 in the vicinity of the inlet 23 in the slow cooling furnace 20 can be set to a desired temperature.
  • the chamber 30 includes a hood 31 provided above the glass ribbon 2, a dross box 32 provided below the glass ribbon 2, and the like.
  • the chamber 30 may have a heat insulating structure.
  • a heat insulating material 33 At least a part of the outer wall of the hood 31 is covered with a heat insulating material 33, and at least a part of the inner wall of the dross box 32 is heat insulating material. 34.
  • a general thing is used as the heat insulating materials 33 and 34.
  • rolls 41 to 43 In the chamber 30, in addition to the lift-out rolls 41 to 43 (hereinafter simply referred to as “rolls 41 to 43”), contact members 44 to 46, a drape 47, a heater 48, and the like are provided.
  • Each of the rolls 41 to 43 is rotationally driven by a driving device such as a motor, and conveys the glass ribbon 2 obliquely upward by the driving force.
  • the number of rolls is not particularly limited as long as it is plural.
  • Contact members 44 to 46 are provided below the rolls 41 to 43.
  • Contact members 44 to 46 are made of carbon or the like.
  • the contact members 44 to 46 are in sliding contact with the outer peripheral surfaces of the corresponding rolls 41 to 43, respectively, and partition the lower space of the glass ribbon 2 into a plurality of spaces 35 to 38.
  • the drape 47 is a member that is provided above the glass ribbon 2 and partitions the upper space of the glass ribbon 2. In the space above the glass ribbon 2, reducing gas that has flowed out from the outlet 13 of the float bath 10 flows toward the inlet 23 of the slow cooling furnace 20.
  • the drape 47 restricts the air from entering from the slow cooling furnace 20 and regulates the increase in the oxygen concentration in the chamber 30. Thereby, combustion of hydrogen in the reducing gas can be suppressed, and temperature fluctuation and local heating due to the hydrogen combustion flame can be suppressed.
  • the drape 47 is made of a refractory material such as steel or glass.
  • the drape 47 is configured to be slightly separated from the upper surface of the glass ribbon 2 so as not to hinder the conveyance of the glass ribbon 2.
  • the drape 47 is suspended by the hood 31 and the heat insulating material 33, and a plurality of the drapes 47 are provided along the conveyance direction of the glass ribbon 2.
  • the heaters 48 are provided separately on the upper and lower sides of the glass ribbon 2 and are provided in a plurality of rows along the conveying direction of the glass ribbon 2.
  • the heaters 48 in each row are provided between the drapes 47 and between the contact members 44 to 46, for example, as shown in FIG.
  • the heaters 48 in each row may be divided in the width direction of the glass ribbon 2.
  • the temperature distribution of the glass ribbon 2 can be precisely adjusted by dividing and arranging the plurality of heaters 48 in the width direction, the conveyance direction, and the vertical direction of the glass ribbon 2 and independently controlling the heat generation amount. It is possible to suppress the warpage of the product.
  • the plurality of heaters 48 may be controlled independently, but some may be controlled together.
  • the manufacturing apparatus 1 of the present embodiment further includes first to fifth air supply pipes 51 to 55.
  • the first to fifth air supply pipes 51 to 55 supply gas into the chamber 30 except for the second air supply pipe 52.
  • the second air supply pipe 52 supplies gas into the slow cooling furnace 20.
  • the first air supply pipe 51 is an inert gas that is a cooling gas in a space 35 downstream of the contact point 4 between the glass ribbon 2 and the most downstream roll 43 in the space below the glass ribbon 2 in the chamber 30. Supply gas. As long as the air supply port of the first air supply pipe 51 is provided below the glass ribbon 2 and downstream of the contact point 4 between the glass ribbon 2 and the most downstream roll 43 in the chamber 30, It may be inside or outside the space 35 (in the side). In the latter case, an inert gas is blown into the space 35 from the outside.
  • the inert gas supplied by the first air supply pipe 51 cools the lower surface of the glass ribbon 2 on the downstream side of the contact point 4 with the most downstream roll 43 by cooling the space 35. Thereby, the temperature of the glass ribbon 2 in the vicinity of the outlet 39 in the chamber 30 can be set sufficiently low, and the warpage of the product can be suppressed.
  • the transition point of the glass is a temperature lower than the annealing point of the glass, and is a temperature at which the viscosity of the glass is 2 ⁇ 10 13 dPa ⁇ s.
  • the glass ribbon 2 since the temperature of the glass ribbon 2 near the outlet 39 in the chamber 30 is set sufficiently low, the glass ribbon 2 can pass through the temperature region near the glass transition point in a short time. Therefore, the influence that the thermal expansion coefficient of the glass rapidly changes at the transition point of the glass can be suppressed, and the warpage of the product can be suppressed.
  • the temperature of the glass ribbon 2 in the vicinity of the outlet 39 in the chamber 30 is appropriately set according to the type of glass, but for example, a temperature in the range of ⁇ 50 to 10 ° C. is preferable based on the annealing point of the glass. A more preferred range is ⁇ 50 to 5 ° C., and a further preferred range is ⁇ 50 to 0 ° C.
  • the first supply pipe 51 may supply the inert gas continuously or intermittently so that the temperature of the glass ribbon 2 in the vicinity of the outlet 39 in the chamber 30 falls within a predetermined temperature range. May be.
  • the present invention is suitable when the thickness of the glass plate as a product is 3 mm or less, suitable for 2 mm or less, more suitable for 1.5 mm or less, and 0.7 mm or less. Is particularly suitable.
  • the thickness of a glass plate it is desirable that it is 0.1 mm or more from a viewpoint of handling property.
  • the glass ribbon 2 downstream from the contact point 4 with the most downstream roll 43 is cooled, when the glass ribbon 2 breaks, the downstream side from the contact point 4 with the most downstream roll 43. Divide by.
  • the subsequent portion of the glass ribbon 2 is already placed on the plurality of rolls 41 to 43, it is easy to convey the subsequent portion toward the slow cooling furnace 20. If the glass ribbon 2 breaks on the upstream side of the most downstream roll 43, the work of passing the succeeding portion of the glass ribbon 2 against the roll 43 obliquely upward against gravity is complicated.
  • the second air supply pipe 52 is a space 26 on the upstream side of the contact 3 between the glass ribbon 2 and the most upstream transport roll 21 in the lower space (or / and the upper space) of the glass ribbon 2.
  • Supply cooling gas to The air supply port of the second air supply pipe 52 is below (or / and above) the glass ribbon 2 and upstream of the contact 3 between the glass ribbon 2 and the most upstream transport roll 21 in the slow cooling furnace 20. As long as it is provided, it may be inside the space 26 or outside the space 26. In the latter case, the cooling gas is blown into the space 26 from the outside.
  • the cooling gas cools the space 26, thereby cooling the lower surface (or / and the upper surface) of the glass ribbon 2 upstream of the contact point 3 with the most upstream transport roll 21. Thereby, the same effect as the case where the temperature of the glass ribbon 2 near the exit 39 in the chamber 30 is set sufficiently low can be obtained.
  • the second supply pipe 52 may supply the cooling gas continuously or intermittently so that the temperature of the glass ribbon 2 in the vicinity of the inlet 23 in the slow cooling furnace 20 falls within a predetermined temperature range. Also good.
  • the third air supply pipe 53 supplies an inert gas to a space 38 upstream of the contact 5 between the glass ribbon 2 and the most upstream roll 41 in the lower space of the glass ribbon 2. .
  • the air supply port of the third air supply pipe 53 is provided below the glass ribbon 2 and upstream from the contact point 5 between the glass ribbon 2 and the most upstream roll 41 in the chamber 30, It may be inside or outside the space 38. In the latter case, an inert gas is blown into the space 38 from the outside. The inert gas cools the lower surface of the glass ribbon 2 upstream of the contact point 5 with the most upstream roll 41 by cooling the space 38.
  • the fourth air supply pipe 54 includes a contact 5 between the glass ribbon 2 and the most upstream roll 41 and a contact 4 between the glass ribbon 2 and the most downstream roll 43 in the lower space of the glass ribbon 2 in the chamber 30.
  • An inert gas is supplied to at least a part of the space 37 between the two.
  • the air supply port of the fourth air supply pipe 54 is located below the glass ribbon 2, downstream from the contact point 5 between the glass ribbon 2 and the most upstream roll 41, and to the glass ribbon 2.
  • it may be inside the space 37 or outside the space 37. In the latter case, the space 37 is inactive from the outside to the inside. Inject gas.
  • the inert gas cools the space 37 to cool at least a part of the lower surface of the glass ribbon 2 between the contact 5 with the most upstream roll 41 and the contact 4 with the most downstream roll 43.
  • the fifth air supply pipe 55 supplies an inert gas downward from the vicinity of the upper wall 14 of the outlet 13 of the float bath 10 in the chamber 30.
  • the inert gas cools the upper surface of the glass ribbon 2 upstream of the contact point 5 with the most upstream roll 41. Further, the inert gas dilutes the hydrogen concentration in the reducing gas flowing out from the float bath 10 to suppress temperature fluctuations and local heating due to the hydrogen combustion flame.
  • the second to fifth air supply pipes 52 to 55 are used in combination with the first air supply pipe 51.
  • the second to fifth air supply pipes 52 to 55 are used in combination with the first air supply pipe 51.
  • the third to fifth supply pipes 52 to 55 may continuously supply an inert gas so that the temperature of the glass ribbon 2 in the vicinity of the outlet 39 in the chamber 30 falls within a predetermined temperature range. You may supply intermittently.
  • an inert gas is used in order to prevent the combustion of hydrogen in the chamber 30 except for the second supply pipe 52.
  • the inert gas include argon gas, but nitrogen gas is desirable from the viewpoint of cost.
  • a nitrogen gas having an oxygen concentration of 1 volume ppm or less is used.
  • a gas containing at least one of air, water vapor, and inert gas is used as the supply gas supplied by the second supply pipe 52.
  • the temperature of the supply gas at each air inlet is preferably 400 ° C. or higher. If the temperature of the supply gas is too low, the glass ribbon 2 may break due to thermal shock. On the other hand, if the temperature of the supply gas is too high, it is difficult to sufficiently cool the glass ribbon 2. Therefore, it is desirable that the temperature of the supply gas at each air supply port is a temperature that is lower by 80 ° C. or more with reference to the temperature of the glass ribbon 2 passing above or below.
  • the flow rates of these supply gases may be automatically controlled based on the temperature distribution in the chamber 30.
  • the temperature in the chamber 30 is detected by a temperature sensor such as a thermocouple, and the detection result is supplied to the control device.
  • the control device controls the opening degree of the electromagnetic valve provided in each of the air supply pipes 51 to 55 based on the detection result of the temperature sensor.
  • the manufacturing apparatus 1 of the present embodiment further includes a detector 62 that detects the breakage of the glass ribbon 2.
  • the detector 62 is provided near the outlet 39 in the chamber 30 or near the inlet 23 in the slow cooling furnace 20. Thereby, the crack of the glass ribbon 2 can be detected at an early stage.
  • the detector 62 may have a general configuration, and may be a mechanical type or an optical type.
  • the detector 62 may be configured by a roller member that is placed on the glass ribbon 2 and drops when the glass ribbon 2 is broken, a position sensor that detects the position of the roller member, and the like.
  • the detector 62 may be configured by a light receiving sensor that irradiates light to the side surface of the glass ribbon 2, receives the reflected light, and detects a crack based on a change in the amount of received light.
  • Example 1 a glass plate having a length of 1800 mm, a width of 1500 mm, and a thickness of 0.7 mm was manufactured using the manufacturing apparatus 1 shown in FIG.
  • glass of this glass plate glass having an annealing point of 711 ° C. was used.
  • Nitrogen gas was used as the gas supplied from the first to fifth supply pipes 51 to 55 shown in FIG. 1 except for the second supply pipe 52. Air was used as the gas supplied from the second air supply pipe 52.
  • the temperature at the center in the width direction of the glass ribbon 2 was measured with a radiation thermometer in each of the vicinity of the outlet 13 in the float bath 10 and the vicinity of the outlet 39 in the chamber 30.
  • the plane strain (residual stress) which is an index of warpage of the glass plate to be manufactured, is the optical path difference of linearly polarized waves orthogonal to each other (optical path difference in the thickness direction of the glass plate) measured by a birefringence measuring instrument. ).
  • Example 1 the temperature of the glass ribbon 2 was 755 ° C. near the outlet 13 in the float bath 10 and 697 ° C. near the outlet 39 in the chamber 30. The glass ribbon 2 was not cracked. The maximum value of the plane strain of the glass plate was 0.95 MPa, and the average value was 0.72 MPa.
  • Comparative Example 1 a glass plate was produced in the same manner as in Example 1 except that no gas was supplied from the first to fifth supply pipes 51 to 55, and the same measurement as in Example 1 was performed. went. The measurement results are shown in Table 1.
  • the temperature of the glass ribbon 2 was 753 ° C. near the outlet 13 in the float bath 10 and 722 ° C. near the outlet 39 in the chamber 30.
  • the glass ribbon 2 was not cracked.
  • the maximum value of the plane strain of the glass plate was 1.71 MPa, and the average value was 1.31 MPa.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Re-Forming, After-Treatment, Cutting And Transporting Of Glass Products (AREA)
  • Glass Compositions (AREA)
PCT/JP2011/073736 2010-11-18 2011-10-14 ガラス板の製造装置およびガラス板の製造方法 WO2012066889A1 (ja)

Priority Applications (4)

Application Number Priority Date Filing Date Title
EP11841009.1A EP2641881A4 (en) 2010-11-18 2011-10-14 DEVICE FOR PREPARING GLASS PANES AND METHOD FOR PRODUCING GLASS PANES
KR1020127018008A KR101223395B1 (ko) 2010-11-18 2011-10-14 유리판의 제조 장치 및 유리판의 제조 방법
CN201180055637.5A CN103221352B (zh) 2010-11-18 2011-10-14 玻璃板的制造装置及玻璃板的制造方法
JP2012523147A JP5838966B2 (ja) 2010-11-18 2011-10-14 ガラス板の製造装置およびガラス板の製造方法

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Application Number Priority Date Filing Date Title
JP2010-258102 2010-11-18
JP2010258102 2010-11-18

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WO2012066889A1 true WO2012066889A1 (ja) 2012-05-24

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PCT/JP2011/073736 WO2012066889A1 (ja) 2010-11-18 2011-10-14 ガラス板の製造装置およびガラス板の製造方法

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EP (1) EP2641881A4 (zh)
JP (1) JP5838966B2 (zh)
KR (1) KR101223395B1 (zh)
CN (1) CN103221352B (zh)
TW (1) TWI527777B (zh)
WO (1) WO2012066889A1 (zh)

Cited By (10)

* Cited by examiner, † Cited by third party
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WO2013187179A1 (ja) * 2012-06-15 2013-12-19 旭硝子株式会社 板ガラスの製造装置、及び板ガラスの製造方法
TWI585051B (zh) * 2012-06-15 2017-06-01 Asahi Glass Co Ltd Production method of plate glass and manufacturing method of plate glass
WO2014069372A1 (ja) * 2012-10-31 2014-05-08 旭硝子株式会社 フロートガラスの製造方法と製造装置
CN104768884A (zh) * 2012-10-31 2015-07-08 旭硝子株式会社 浮法玻璃的制造方法和制造装置
CN104837782A (zh) * 2012-11-16 2015-08-12 旭硝子株式会社 浮法平板玻璃制造装置、浮法平板玻璃制造方法
WO2014103478A1 (ja) * 2012-12-28 2014-07-03 旭硝子株式会社 徐冷装置、徐冷方法、ガラス板の製造装置、及びガラス板の製造方法
US10392289B2 (en) 2013-10-31 2019-08-27 AGC Inc. Method for manufacturing float glass, and float glass
JPWO2015064595A1 (ja) * 2013-10-31 2017-03-09 旭硝子株式会社 フロートバス用錫合金浴、フロートガラスの製造装置、フロートガラスの製造方法、および、フロートガラス
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WO2015064595A1 (ja) * 2013-10-31 2015-05-07 旭硝子株式会社 フロートバス用錫合金浴、フロートガラスの製造装置、フロートガラスの製造方法、および、フロートガラス
WO2015093432A1 (ja) * 2013-12-18 2015-06-25 旭硝子株式会社 フロートガラス製造装置、およびフロートガラス製造方法
KR20160119497A (ko) 2015-04-06 2016-10-14 아사히 가라스 가부시키가이샤 플로트 유리의 제조 장치
KR20180030579A (ko) * 2015-08-10 2018-03-23 쌩-고벵 글래스 프랑스 박형 유리 층의 절단 방법
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KR102077667B1 (ko) 2015-08-10 2020-02-14 쌩-고벵 글래스 프랑스 박형 유리 층의 절단 방법
US10759690B2 (en) 2015-08-10 2020-09-01 Saint-Gobain Glass France Method for cutting a thin glass layer
US20210061697A1 (en) * 2018-05-17 2021-03-04 AGC Inc. Float glass production device and float glass production method
US11760679B2 (en) * 2018-05-17 2023-09-19 AGC Inc. Float glass production device and float glass production method
CN113683300A (zh) * 2021-08-25 2021-11-23 四川虹科创新科技有限公司 一种带有工艺补偿的自动稳定锡槽渣箱

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